ANNEXURE Annexure 1: Production Details Annexure 2: Site Location Map Annexure 3: Site Layout Map & Area breakup for Terminal Annexure 4: Operation Philosophy Annexure 5: Copy of Consent to Operate Annexure 6: Storage tank Details Annexure 7: Water consumption & Waste water generation details Annexure 8: Fuel consumption details Annexure 9: Hazardous waste generation details Annexure 10: Stack details Annexure 11: Land Possession documents
Annexure 1: Production Details Table 0-1: Details of Existing & Additional Chemicals Storage Material HSD MS SKO Storage Capacity (KL) Existing Additional Total Nos. of Storage Tanks Storage Capacity (KL) Nos. of Storage Tanks 11000 1 - - 13791 1 - - 10805 1 - - 6800 1 - - 9163 1 - - 8827 1 - - 6981 2 - - 8385 2 - - 5230 1 - - Storage Capacity (KL) Nos. of Storage Tanks 42396 4 31952 4 13615 3 LDO 5200 1 - - 5200 1 ATF 16220 2 - - 8655 1 - - 7194 1 - - 9783 1 - - 4000 1 - - 62072 6 EMPTY 180 2 - - 360 2 93-OCTANE 180 1 - - 180 1 ETHANOL 938 2 2000 2 5876 4 Total storage quantity (KL) 166036 23 4000 2 170036 25
Annexure 2: Site Location Map
Sr. No. Point Latitude Longitude 1 A 28 32'15.97"N 77 3'37.31"E 2 B 28 32'18.01"N 77 3'35.83"E 3 C 28 32'26.19"N 77 3'18.41"E 4 D 28 32'37.89"N 77 3'27.97"E 5 E 28 32'31.67"N 77 3'43.50"E 6 F 28 32'29.18"N 77 3'43.31"E 7 G 28 32'26.39"N 77 3'40.98"E 8 H 28 32'28.37"N 77 3'36.88"E 9 I 28 32'21.18"N 77 3'31.65"E 10 J 28 32'18.92"N 77 3'35.51"E 11 K 28 32'16.96"N 77 3'38.70"E
Annexure 3: Site Layout Map
The Total site area is 71 Acres. The area details of the existing facility and the additional facilities are given below in the Table. Table 0-2: Area breakup for terminal S. no. Description Area, m 2 (Tentative) % of Total Area 1 Storage tank farm area (existing) 53608 18.7 2 Storage tank farm area (additional) 4547 1.6 3 Utility area (FE/PH, PH) 1161 0.4 4 Administrative Building 600 0.2 5 Building Blocks 6515 2.3 6 Parking 240 0.1 7 Roads 5270 1.8 8 Green belt area 16721 5.8 9 Fire water storage area 1325 0.5 10 Loading Unloading area 2446 0.9 11 Misc ( TLF, Open space, scrap yard, lube oil, TT Parking, Officers coloney etc ) 194894 67.8 Total 287327 100.0
Annexure 4: Operation Philosophy Delhi Terminal, Bijwasan is a Petroleum Product Storage Terminal of Indian Oil Corporation Limited, located in New Delhi, the Capital City of Republic of India. The terminal operates in 3 shifts and its activity involves receipt, storage and distribution of finished petroleum product (Motor Gasolene, Gas Oil and Aviation Fuel). The product is received from Mathura & Panipat Refineries through cross country pipelines. There is a provision to receive LDO & Aviation Fuel through Tank Wagons as well. For storage of various products, Delhi Terminal has 23 Storage Tanks. Delivery of product to various customers is undertaken through pipelines as well as Tank Lorries. The Terminal also handles Ethanol, which is mixed in a proportion of 10% by volume with Motor Gasoline for dispatches. At Bijwasan terminal product inlet is through Mathura Jalandhar pipeline which has commenced on 27 th April 1982 & is around 763 kms in length. This pipeline runs around 147 kms from Mathura to Delhi with a capacity of about 3.70 MMTPA. Storage capacity of terminal is 165720 KLs with 23 tanks storing different products. On an average 400 T/T were loaded per day with the help of TLF Gantry with 30 loading bays & 23 pumps for different products at the terminal The Terminal is operated in accordance with the provisions of licenses and consents granted by regulatory departments viz. Departments of Petroleum & Explosives Safety Organization, Directorate of Factories, Manufacture, Storage & Import of Hazardous Chemical Rules & Pollution Control Board etc. as per the applicable regulatory statutory acts and rules of Govt. of India. 1.1.1 Activities at Terminal Tank Lorry Loading - MS, HSD, SKO, ATF, LDO Tank Lorry Unloading : MS, 93 Octane, SKO, Ethanol Ethanol blending, at TLF Loading of additive to the additive tank and blending at TLF Pipeline Receipt through Cross Country Pipeline MS, HSD, SKO & ATF Receipt through Tank Wagon (Intermittent) ATF, LDO Inter tank transfer Tank Water Draining Operation Sampling of Product from Tank after every receipt Emptying out of Tank at fixed interval for Maintenance/ Cleaning for Quality Control adherence Opening of Strainers for Cleaning of Strainer s Filters at fixed interval. Maintenance and Repair of various Equipments Viz. Pumps, Motors, Fire Engines, Air Compressors etc. Process Flow Diagram of the operation at Terminal is enumerated as under:
Figure 3.1: Process Flow Diagram 1.1.2 Ethanol blending process Nominate the ETHANOL Tank (TK-21 or TK-22) for MS- Ethanol blending at TLF. Nominate the ETHANOL Pump (E1 OR E2) for pumping ETHANOL to TLF through the nominated ETHANOL Tank (TK-21 or TK-22). Carry out gauging of the tanks and upload the gauges in SAP. Check line up of the nominated tanks & pumps or pump sequence for TLF Operation, by opening valves which are numbered for Operating sequence as below.
Figure 3.2: Ethanol blending process
Annexure 5: Copy of Consent to Operate
Annexure 6: Storage tank details S. No. Tank No. Material Physical State Hazard Involve Storage Capacity (KL) Type of Tank (CR/FR/UG /AG/SB) Height (m) Dia (m) Operating Condition Press Kg/Cm 2 Temp ºC 1 TK1 HSD Liquid Flammable 11000.00 CR 13.75 M 36.00 Atmospheric Ambient 2 TK2 HSD Liquid Flammable 13791.00 CR 14.00 M 36.00 Atmospheric Ambient 3 TK3 HSD Liquid Flammable 10805.00 CR 14.00 M 32.00 Atmospheric Ambient 4 TK4 MS Liquid Flammable 9163.00 FR 12.93 M 32.00 Atmospheric Ambient 5 TK5 MS Liquid Flammable 8827.00 FR 12.48 M 32.00 Atmospheric Ambient 6 TK6 SKO Liquid Flammable 5230.00 CR 14.33 M 22 Atmospheric Ambient 7 TK7 LDO Liquid Flammable 5200.00 CR 14.34 M 22 Atmospheric Ambient 8 TK8 HSD Liquid Flammable 6800.00 CR 13.41 M 26 Atmospheric Ambient 9 TK9 ATF Liquid Flammable 16220.00 CR 14.93 M 38 Atmospheric Ambient 10 TK10 ATF Liquid Flammable 16220.00 CR 15.00 M 38 Atmospheric Ambient 11 TK11 MS Liquid Flammable 6981.00 FR 16.50 M 24 Atmospheric Ambient 12 TK12 MS Liquid Flammable 6981.00 FR 16.50 M 24 Atmospheric Ambient 13 TK13 ATF Liquid Flammable 8655.00 CR 14.75 M 28 Atmospheric Ambient 14 TK14 ATF Liquid Flammable 7194.00 CR 14.55 M 26 Atmospheric Ambient 15 TK15 ATF Liquid Flammable 9783.00 CR 14.55 M 30 Atmospheric Ambient 16 TK16 SKO Liquid Flammable 8385.00 CR 15.00 M 28 Atmospheric Ambient 17 TK17 SKO Liquid Flammable 8385.00 CR 15.00 M 28 Atmospheric Ambient 18 TK18 EMPTY Liquid Flammable 180.00 SB 16.25 M(L) 3.75 Atmospheric Ambient 19 TK19 EMPTY Liquid Flammable 180.00 SB 16.25 M(L) 3.75 Atmospheric Ambient 20 TK20 93-OCTANE Liquid Flammable 180.00 SB 16.25 M(L) 3.75 Atmospheric Ambient 21 TK21 ETHANOL Liquid Flammable 938.00 CR 12.00 M 10 Atmospheric Ambient 22 TK22 ETHANOL Liquid Flammable 938.00 CR 12.00M 10 Atmospheric Ambient 23 TK24 ATF Liquid Flammable 4000.00 CR 14.70 M 20 Atmospheric Ambient
Annexure 7: Water consumption & Waste water generation details Water will be sourced through Tankers. As the terminal is providing only storage and handling services, there is no additional water requirement for processing or operation, water is required only for gardening and domestic purpose. Terminal s existing water requirement is 50 KLD. After addition of two new tanks, domestic water consumption will not increase. So after proposed expansion water consumption will remain same as 50 KLD. Table 0-3: Water Consumption Details S. No. Description Water Consumption in KLD Existing Additional Total 1 Processing 0 0 0 2 Gardening 10 0 10 3 Domestic 40 0 40 Total 50 0 50 There will not be any generation of industrial effluent. Domestic wastewater will be disposed off in soak pit through septic tank. Break up of wastewater generation along with disposal mode is given in following table Table 0-4: Wastewater Generation and disposal S. No. Description Wastewater Generation in KLD Existing Additional Total Disposal Mode 1 Industrial Operation 0 0 0-2 Gardening 0 0 0-3 Domestic 20 0 20 Total 20 0 20 To send to Septic Tank
Annexure 8: Fuel consumption details Table 0-5: Fuel Consumption details Sr. No. Stack Attached to Capacity Stack Nos. Type of Fuel used Fuel consumption Existing 1 DG set 2 x 750 KVA + 1 x 500 KVA 5 HSD 140 Ltr/hr. at full load 2 Fire water Engine pumps 8 x 616 m 3 8 HSD 35 Ltr/hr. at full load Additional No flue gas stack will be added after additional tankage
Annexure 9: Hazardous waste generation details Table 0-6: Hazardous waste Generation and disposal S. No. Hazardous Waste Hazardous Waste Category Quantity in MTPA Existing Proposed Total 1 Used Oil 5.1 60 liters 0.00 60 liters 2 Tank cleaning Sludge Management Disposed to authorized agency 3.3 0.6 0.02 0.62 Internal Bio- remedial
Annexure 10: Stack details Table 0-7: Stack details Sr. No. 1 2 Stack Attached to Capacity Stack Nos. DG set As a backup during emergency Fire water Engine pumps Existing Stack Height, m Stack Top Dia, m 2 X 750 KVA 4 7 6 inch 1 X 500 KVA 1 7 6 inch 8 X 616 m3 8 7 6 inch Proposed No flue gas stack will be added after proposed expansion
Annexure 11: Land possession documents